合成生物学 ›› 2024, Vol. 5 ›› Issue (6): 1404-1418.DOI: 10.12211/2096-8280.2024-032
程峰1,2, 邹树平1,2, 徐建妙1,2, 汤恒1,2, 薛亚平1,2, 郑裕国1,2
收稿日期:
2024-04-02
修回日期:
2024-06-25
出版日期:
2024-12-31
发布日期:
2025-01-10
通讯作者:
薛亚平
作者简介:
基金资助:
Feng CHENG1,2, Shuping ZOU1,2, Jianmiao XU1,2, Heng TANG1,2, Yaping XUE1,2, Yuguo ZHENG1,2
Received:
2024-04-02
Revised:
2024-06-25
Online:
2024-12-31
Published:
2025-01-10
Contact:
Yaping XUE
摘要:
草铵膦是全球三大除草剂之一,具有广谱、高活性、非选择性等特点,市场前景被广泛看好。然而,草铵膦具有两种对映异构体(
中图分类号:
程峰, 邹树平, 徐建妙, 汤恒, 薛亚平, 郑裕国. 生物高纯精草:高光学纯L-草铵膦生物制造的创新与发展[J]. 合成生物学, 2024, 5(6): 1404-1418.
Feng CHENG, Shuping ZOU, Jianmiao XU, Heng TANG, Yaping XUE, Yuguo ZHENG. BioHPP®: a benchmark of biomanufacturing for high optically pure L-phosphinothricin[J]. Synthetic Biology Journal, 2024, 5(6): 1404-1418.
条目 | 热裂解-ACA工艺(“气相合成”) | 铝法-Strecker工艺(“铝法合成”) | 格氏-Strecker工艺(“格氏合成”) |
---|---|---|---|
连续化程度 | 完全连续化 | 半连续化 | 间歇化 |
工艺特点 | 连续化程度高 对反应器装置要求高 | 工艺简单 易燃易爆,使用剧毒氰化物,分离纯化困难 | 工艺简单 易燃易爆,使用剧毒氰化物,分离纯化困难 |
三废排放 | 固废量少,可用来制备高附加值产品 | 固废量大 | 废水量大 |
生产成本 | 5万~6万 元/吨 | 6万~7万 元/吨 | 7万~8万元/吨 |
表1 D,L-草铵膦三种生产工艺比较
Table 1 Comparison of three production processes for D,L-PPT
条目 | 热裂解-ACA工艺(“气相合成”) | 铝法-Strecker工艺(“铝法合成”) | 格氏-Strecker工艺(“格氏合成”) |
---|---|---|---|
连续化程度 | 完全连续化 | 半连续化 | 间歇化 |
工艺特点 | 连续化程度高 对反应器装置要求高 | 工艺简单 易燃易爆,使用剧毒氰化物,分离纯化困难 | 工艺简单 易燃易爆,使用剧毒氰化物,分离纯化困难 |
三废排放 | 固废量少,可用来制备高附加值产品 | 固废量大 | 废水量大 |
生产成本 | 5万~6万 元/吨 | 6万~7万 元/吨 | 7万~8万元/吨 |
图4 通用化合物氰基化再水解路线合成L-草铵膦路线图与腈水解酶工业适配
Fig. 4 Diagram of L-PPT synthesis route via cyanation and hydrolysis of general compounds and industrial adaptation of nitrilase
条目 | 通用化合物氰基化再水解路线 | 外消旋 混旋体合成-去消旋化路线 | 从常用化学品合成 | 从头合成高丝氨酸再化学合成路线 | |||
---|---|---|---|---|---|---|---|
生物拆分 | 生物有机胺胺化 | 生物无机氨胺化 | 生物无机氨胺化 | 生物有机胺胺化 | |||
生物 催化剂 | 腈水解酶等 | 酰化酶、酰胺酶等 | 氧化酶/多个转氨酶 | 脱氢酶等 | 转氨酶 | 生物发酵 | |
供体 | 无 | 无 | 3~4倍当量有机胺 | 无机氨 | 无机氨 | 2~4倍当量有机胺 | 有机膦 |
底物 | 氨基腈 | 草铵膦衍生物 | 潜手性酮 | 葡萄糖 | |||
转化率 产物e.e.值 | 86% >99% | <50% >99% | 90%~99% >99% | 100% >99% | <100% >99% | 90%~99% >99% | >99% |
分离 纯化 | 容易 | 容易 | 困难 | 容易 | 容易 | 困难 | 容易 |
(原粉、水剂) | (原粉、水剂) | (水剂) | (原粉、水剂) | (原粉、水剂) | (水剂) | (原粉、水剂) |
表2 L-草铵膦四大技术路线比较
Table 2 Comparison of four technical routes for L-PPT
条目 | 通用化合物氰基化再水解路线 | 外消旋 混旋体合成-去消旋化路线 | 从常用化学品合成 | 从头合成高丝氨酸再化学合成路线 | |||
---|---|---|---|---|---|---|---|
生物拆分 | 生物有机胺胺化 | 生物无机氨胺化 | 生物无机氨胺化 | 生物有机胺胺化 | |||
生物 催化剂 | 腈水解酶等 | 酰化酶、酰胺酶等 | 氧化酶/多个转氨酶 | 脱氢酶等 | 转氨酶 | 生物发酵 | |
供体 | 无 | 无 | 3~4倍当量有机胺 | 无机氨 | 无机氨 | 2~4倍当量有机胺 | 有机膦 |
底物 | 氨基腈 | 草铵膦衍生物 | 潜手性酮 | 葡萄糖 | |||
转化率 产物e.e.值 | 86% >99% | <50% >99% | 90%~99% >99% | 100% >99% | <100% >99% | 90%~99% >99% | >99% |
分离 纯化 | 容易 | 容易 | 困难 | 容易 | 容易 | 困难 | 容易 |
(原粉、水剂) | (原粉、水剂) | (水剂) | (原粉、水剂) | (原粉、水剂) | (水剂) | (原粉、水剂) |
酶类 | 国际酶学编号 | 辅酶再生底物 | 辅酶再生产物 | 优点 | 缺点 |
---|---|---|---|---|---|
FDH | EC 1.2.1.2 | 甲酸(铵) | CO2和水 | 副产物CO2无毒具挥发性易于分离 | 催化效率低,底物亲和力差,具NAD+特异性 |
GDH | EC 1.1.1.47 | 葡萄糖 | 葡萄糖酸 | 催化活力高,辅底物价格低廉 | 副产物易溶于水难以分离,反应pH降低需要调控 |
ADH | EC 1.1.1.1-2 | 异丙醇 | 丙酮 | 催化活力较高,副产物沸点低,易除去 | 反应可逆,副产物可能会影响酶活 |
表3 辅酶再生酶的分类及特点
Table 3 Classification and characteristics of coenzyme regeneration enzymes
酶类 | 国际酶学编号 | 辅酶再生底物 | 辅酶再生产物 | 优点 | 缺点 |
---|---|---|---|---|---|
FDH | EC 1.2.1.2 | 甲酸(铵) | CO2和水 | 副产物CO2无毒具挥发性易于分离 | 催化效率低,底物亲和力差,具NAD+特异性 |
GDH | EC 1.1.1.47 | 葡萄糖 | 葡萄糖酸 | 催化活力高,辅底物价格低廉 | 副产物易溶于水难以分离,反应pH降低需要调控 |
ADH | EC 1.1.1.1-2 | 异丙醇 | 丙酮 | 催化活力较高,副产物沸点低,易除去 | 反应可逆,副产物可能会影响酶活 |
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